Low Emission, High Scrub VAE Latex Paints

ABSTRACT

A water-based, low-emission latex paint formulation includes a vinyl acetate/ethylene (VAE) latex including a VAE resin with from 80 to 95 weight % vinyl acetate residue and from 5 to 20 weight % ethylene residue, optionally including additional monomers as well as a pigment composition including inorganic solids selected from inorganic pigments, inorganic fillers and mixtures thereof present in an amount such that the paint formulation has a pigment volume concentration (PVC) of from 25% to 85%. The formulations are suitable for eggshell and flat latex paints and exhibit surprising durability.

CLAIM FOR PRIORITY

This application is a continuation of U.S. patent application Ser. No.12/584,152, filed Sep. 1, 2009. U.S. patent application Ser. No.12/584,152 claimed the benefit of the filing date of U.S. ProvisionalPatent Application Ser. No. 61/190,727, of the same title, filed Sep. 2,2008. The priorities of U.S. patent application Ser. No. 12/584,152 andU.S. Provisional Patent Application Ser. No. 61/190,727 are herebyclaimed and the disclosures thereof are incorporated into thisapplication by reference.

FIELD OF INVENTION

This invention relates to water-based, low-emission latex paintformulations including a vinyl acetate/ethylene (VAE) latex andinorganic solids present in an amount such that the paint formulationhas a pigment volume concentration (PVC) of from 25% to 85%. Theseformulations are suitable for eggshell and flat latex interior paints.

BACKGROUND OF THE INVENTION

There are numerous references which describe latex paint compositionsincorporating a vinyl acetate-ethylene emulsion as a binder.Representative patents include U.S. Pat. Nos. 3,404,112 and 3,404,113.The '112 patent discloses the use of vinyl acetate-ethylene latexes as afilm-forming binder in an aqueous paint composition. The '113 patentincorporates a triallylcyanurate in the polymerization process toenhance the degree of insolubles. The particle size of the binder willrange from about 0.1 to 2 microns. The ethylene content will rangegenerally from 5 to 40, preferably about 10-15% by weight of thepolymer.

U.S. Pat. No. 3,440,199 to Lindemann et al. discloses aqueous paintcompositions incorporating an inter polymer of vinyl acetate, ethyleneand glycidyl acrylate. The addition of the glycidyl acrylate into thepolymer system enhances adhesion to raw wood without the use of a primercoat.

U.S. Pat. No. 4,219,454 to Iacoviello, et al. discloses the use of avinyl acetate copolymer emulsion for preparing semi-gloss and flatinterior paint compositions. Vinyl acetate-ethylene emulsions weredisclosed with preferred latexes having a particle size such that lessthan 5% of the particles had a size greater than 0.65 microns and lessthan 5% had a particle size of less than 0.33 microns. Emulsions wereprepared by introducing the monomers of vinyl acetate, optionally with asmall amount of butyl acrylate into a stabilizer system of water,hydroxyethyl cellulose and multiple nonionic surfactants. The T_(g) ofthe vinyl acetate ethylene polymer was approximately 22° C., preferredlevels of ethylene from about 10 to 15% by weight.

U.S. Pat. No. 5,470,906 to Craun, et al. discloses an aqueous ambientdry paint coating incorporating an emulsion copolymerized additionpolymer containing an oligomer selected from polyurethane or polyesterhaving a T_(g) below about −20° C. and a number average molecular weightbetween 300 and 5,000. The coating is free of organic coalescingsolvents. Vinyl acetate and butylacrylate (80/20) are disclosed asconventional polymeric binders for consumer based paints with the binderhaving an elevated T_(g) lowered temporarily through the use of avolatile coalescing solvent. Low molecular weight oligomers of urethanesand polyester urethane copolymers were used in place of conventionalcoalescing solvents to achieve desired properties without objectionableodor and VOCs.

U.S. Pat. No. 3,969,296 to Wassenburg, et al. discloses a process forproducing a vinyl acetate emulsion having improved adhesioncharacteristics against usual wet-cleaning with a cloth, sponge, etc.The emulsion is prepared by copolymerizing a small amount of a glycidylester of an alpha-beta ethylenically unsaturated acid with vinyl acetatefollowed by neutralization with ammonia.

U.S. Pat. No. 3,563,944 to Bauer et al. discloses a colloid-free vinylacetate emulsion suited for producing paint formulations having goodscrub resistance, film forming properties, mechanical stability, etc.The copolymer consists of vinyl acetate and a lower alkyl acrylate, oran alkyl maleate. Enhanced stability is imparted by polymerizing aportion of the monomers in a colloid-free aqueous medium and then addingmore monomer during the course of reaction and using a nonionicsurfactant to stabilize the polymerization.

The need today for architectural coating materials free from volatileorganic content (VOC) for both safety and health reasons is welldocumented.

Latex paint compositions have captured a significant portion of theindoor and outdoor paint market because they have significant advantagesas compared with organic solvent based paints. Three of the mostimportant advantages are: cleanup is easier with latex paints than withsolvent based paints; there is substantially less air pollutionassociated with latex paints as opposed to solvent based paints; andfire hazards from paint thinners and other solvents needed with solventbased paints are eliminated using latex paints. On the other hand, thecoating properties and storage stability of latex paints have beensomewhat inferior to those of the solvent type, particularly inobtaining desired film thickness, durability and adhesion. This isespecially so in more modestly priced latex products with higher PVC.

Although a significant reduction or elimination of volatile organicsolvents is achieved through the use of latex products, the surfactantsremaining after water evaporation, coupled with the relatively highmolecular weight of the polymers, frequently prevent completecoalescence, which is needed for superior durability, for example, scrubresistance. Conventional vinyl acetate based latex vehicles oftenrequire coalescing solvents in order for the latex to be suitable foruse in a paint formulation. Coalescing solvents are incorporated intothe paint composition to externally and temporarily plasticize the latexpolymer for a time sufficient to develop film formation. This providesvolatile organics, which are undesirable. That is, coalescing solventsdiffuse out of the film after film formation and thus contribute to theVOC level emitted to the environment. Paints formulated with standardvinyl-acrylic latex vehicles and no coalescing solvent generally do notpass the requirement of film formation at temperatures as low as 40° F.Such paints also display cracking upon drying and provide poordurability. One approach to attempt to overcome these deficiencies is toincrease the acrylate level to lower the minimum film formationtemperature of the latex. In particular, acrylate monomers that lower Tgare effective, such as butyl acrylate. Although the approach addressesthe cracking and durability problems, paints prepared from these latexesare more costly and they also display dirt pickup, due to unacceptabletackiness after drying. Therefore, one goal is to prepare a latex whichpermits a low film formation temperature without causing the dried filmto become tacky and to have sufficient hardness to retain gooddurability.

Alkylphenol ethoxylates (APEs) represent a class of nonionic surfactantswhich are used in latex products to improve adhesion and film forming,and in paint formulations to provide pigment wetting. These compoundsare believed to break down in the environment to related compounds thatare persistent in the environment and act as endocrine disruptors. Duein part to regulations in Europe, as well as recently adopted waterquality criteria in the United States, there is a need to use APE-freepolymer emulsion binders in preparation of APE-free paint formulations.The evolving environmental controls of APEs are reminiscent of the 1970sban on lead compounds in paint, enacted to prevent serious health risks,especially to children.

Conventional polymeric binders used in latex paint formulations aretypically emulsion polymers containing surfactants that are based onalkylphenol ethoxylates. Previously known emulsion polymeric bindersthat are free of alkylphenol ethoxylates have not been popular, becausethey do not provide the necessary adhesion, perform more poorly asemulsifiers, and provide poorer color acceptance.

While the art is replete with formulations for latex paints, existingproducts, especially low-emission products, do not exhibit preferredcharacteristics in terms of film forming, durability, adhesion, or stainresistance and often include undesirable components, such as alkylphenolethoxylates.

SUMMARY OF THE INVENTION

There is provided in accordance with this invention water-based,low-emission latex paint formulations including a vinyl acetate/ethylene(VAE) latex and inorganic solids present in an amount such that thepaint formulation has a pigment volume concentration (PVC) of from 25%to 85%. These formulations are suitable for eggshell and flat latexinterior paints and are surprisingly durable, stain resistant and aresuperior film-formers. The paint formulations are based on a new classof APE-free resins available from Celanese Emulsion Polymers, Houston,Tex., and are designated EcoVAE® 405 Series, or may be obtained bysimply requesting high-scrub VAE resin, or requesting suitable resinsusing like terminology.

Without intending to be bound by any particular theory, it is believedthat the paint properties are due to the selection of components,including the VAE latexes from Celanese which may include much moreuniform film formation in the latex than conventional VAE latexes,providing for elevated scrub values and other improvements describedherein. Particularly preferred latexes tend to gel when cured atelevated temperatures, indicating toughness of the compositions.

BRIEF DESCRIPTION OF THE DRAWINGS

The invention is described in detail below with reference to theappended drawings, wherein like numerals designate similar parts. In theFigures:

FIG. 1 is a schematic illustration of pigment volume concentration atvarious levels, a characteristic of paint formulations;

FIG. 2 is a visual example illustrating scrub resistance measurementaccording to ASTM Method D2486-06;

FIG. 3 is a graphical representation comparing scrub resistance of paintformulations containing commercially available resins;

FIG. 4 is a visual example illustrating a dye stain test; and

FIG. 5 is a diagram showing a correlation between K-values and G′(storage modulus) values.

DETAILED DESCRIPTION OF THE INVENTION

The invention is described in detail below with reference to severalembodiments and numerous examples. Such discussion is for purposes ofillustration only. Modifications to particular examples within thespirit and scope of the present invention, set forth in the appendedclaims, will be readily apparent to one of skill in the art. Terminologyused herein is given its ordinary meaning consistent with the exemplarydefinitions set forth immediately below.

In testing procedures discussed herein, unless otherwise noted, ambientconditions are specified.

The term “latex” is used herein in its conventional meaning, i.e., adispersion of particulate matter in an aqueous phase which contains anemulsifier or surfactant suitable for preparing the latex. Latexbinders, as used herein, comprise a polymer dispersed in an aqueousphase with an appropriate emulsifier system. A resin or binder gives thepaint adhesion to the substrate, and seals and protects the substrate.

The term water-based, as used herein, refers to the aqueous phase inwhich the resin is dispersed.

The term glass transition temperature (T_(g)) is used herein in itsconventional meaning; i.e., the temperature at which a polymer changesfrom hard and brittle to soft and pliable at a midpoint fromDifferential Scanning calorimetry (DSC) measurement with a heating rateof 10 K per minute. In other words, on a curve of temperature versusmodulus, the temperature at which a polymer is at the midpoint oftransition from hard and brittle to soft and pliable is referred to asthe glass transition temperature. Increasing a binder T_(g) results inimproved hardness and, therefore, block resistance of a coating film.The ability of a polymer to deform and to bridge the film-film interfacedecreases with increasing T_(g). T_(g) differs from minimum film formingtemperature (MFFT) in that MFFT reflects the ability of a product toform a film without coalescent, whereas T_(g) reflects the filmtoughness of a product. Toughness is a measure of the maximum amount ofenergy a material can absorb before failure occurs. A tougher film ismore resistant to abrasion force. The T_(g) determines the MFFT and thephysical characteristics of a film formed by a polymer. The MFFT isusually lower than T_(g) and the differential is dependent on the degreeof polymer plasticization by water. The gap between T_(g) and MFFT istypically greater for a VAE latex than for an acrylic latex. Althoughnot intending to be bound by theory, this presumably is due to a highpercentage of hydrophilic vinyl acetate monomer present.

Pigment Volume Concentration (PVC) measures the volume contribution ofpigment to the paint. A graphical representation of the effect of PVC isshown in FIG. 1. PVC is calculated according to the following formula.

${{PVC}\mspace{14mu} (\%)} = {\frac{{{Volume}\mspace{14mu} {of}\mspace{14mu} {{Pigment}(s)}} + {{Volume}\mspace{14mu} {of}\mspace{14mu} {{Extender}(s)}}}{\begin{pmatrix}{{{Volume}\mspace{14mu} {of}\mspace{14mu} {{Pigment}(s)}} + {{Volume}\mspace{14mu} {of}\mspace{14mu} {{Extender}(s)}} +} \\{{Volume}\mspace{14mu} {of}\mspace{14mu} {Solid}\mspace{14mu} {{Binder}(s)}}\end{pmatrix}}100}$

Volume solids measures the amount of actual coating that will remain ona wall after application; i.e., after the coating has dried. Whenadditives are present, their volume is not included in determining thetotal dry volume. Volume solids is calculated according to the followingformula.

${{Volume}\mspace{14mu} {solids}\mspace{14mu} (\%)} = {\frac{\begin{matrix}{{{dry}\mspace{14mu} {volume}\mspace{14mu} {of}\mspace{14mu} {{pigment}(s)}} + {{dry}\mspace{14mu} {volume}\mspace{14mu} {of}\mspace{14mu} {{extender}(s)}} +} \\{{dry}\mspace{14mu} {volume}\mspace{14mu} {of}\mspace{14mu} {{binder}(s)}}\end{matrix}}{{total}\mspace{14mu} {volume}\mspace{14mu} {of}\mspace{14mu} {formulation}}100}$

The term low-emission paint formulation, as used herein, refers to apaint formulation with a Volatile Organic Content (VOC) of less than 100g/L. Volatile Organic Content of a paint formulation refers to thepresence of volatile organic components; i.e., any volatile componentthat contains carbon and is not listed by the EPA as an exempt solvent.VOC sources may include co-solvents, including glycols, which help withwet edge application, open time, and freeze—thaw resistance, andcoalescents, which help the latex polymer form a film by lowering T_(g)as the film dries; emulsion components and most additives at low levels.For instance, amino methyl propanol is a volatile compound used toadjust pH. Volatile Organic Content is calculated by the followingformula.

${{Volatile}\mspace{14mu} {Organic}\mspace{14mu} {Content}} = \frac{{Weight}\mspace{14mu} ({grams})\mspace{14mu} {of}\mspace{14mu} {VOC}}{\begin{pmatrix}{{{Total}\mspace{14mu} {Volume}\mspace{14mu} ({Liters})\mspace{14mu} {of}\mspace{14mu} {formula}} -} \\{{{Volume}\mspace{14mu} {of}\mspace{14mu} {Water}} - {{Volume}\mspace{14mu} {of}\mspace{14mu} {Exempt}\mspace{14mu} {Solvents}}}\end{pmatrix}}$

Commercially available latex paints may have VOC levels higher than 150g/L. In contrast, a paint formulation according to the invention mayhave a very low volatile organic content, such as less than 5 g/L.

Key parameters important to the customer include T_(g), particle size,viscosity, stability, and robustness.

Robustness can be determined in part by evaluating “scrub resistance” orscrubbability, the resistance of wall paints to erosion caused byscrubbing. Scrub resistance is measured using ASTM D2486-06, “StandardTest Methods for Scrub Resistance of Wall Paints,” an example of whichis shown in FIG. 2. These test methods determine the relative resistanceof different paints to erosion when repeatedly scrubbed during the lifeof the paint. Test Method A measures scrub resistance by the traditionalcycles-to-failure concept. In an attempt to improve reproducibility,Test Method B was developed. Test Method B provides a ratio, expressedas a percentage, of cycles-to-failure obtained on the test paint to thatobtained on a concurrent run with a known reference paint. This value isrepresented herein as “relative scrub index.” A graphical example ofcomparative scrub resistance is shown in FIG. 3. Note the percentageerror allowed for in Test Method B, reproduced as follows:

-   -   11.1.3 On the basis of an interlaboratory study in which        operators in five laboratories tested five coatings, including        both flat and semi-gloss coatings, the following criteria should        be used for judging the acceptability of the results at the 95%        confidence level:    -   11.1.3.1 Repeatability—Two results (each the mean of duplicate        measurements) obtained by the same operator should be considered        suspect if they differ more than 25% of their mean value.    -   11.1.3.2 Reproducibility—Two results (each the mean of duplicate        measurements) obtained by operators in different laboratories        should be considered suspect if they differ by more than 58% of        their mean.

In FIG. 3, Resyn® 7480 refers to a vinyl acetate/acrylate copolymeremulsion available from Celanese Emulsion Polymers, Houston, Tex. Theresults of these tests are directly related to the polymer quality.Great scrub durability allows a paint formulator to use less binder (inhigher PVC paints) while maintaining acceptable performance. Scrubdurability is related to toughness and elasticity of a coating film.Compared to acrylic, a VAE latex film typically displays highermechanical strength manifested by higher modulus and tensile strength.Compared to acrylic latices, a VAE latex also typically exhibits a lowerrubbery plateau modulus and a higher tan delta peak in the Tg region,suggesting greater ability of a VAE polymer to deform under stress byviscous flow.

Blocking refers to the relative tackiness of a dry coating. It isdesirable that two dry, coated surfaces when placed in contact do notblock or stick together. Conventional knowledge would suggest that VAEcopolymers would generally not have exceptional block resistance, givenlow T_(g) values. Block resistance is also a function of film surfaceproperties. One skilled in the art of emulsion polymerization can altersurface properties by adjusting monomer composition, particlestabilization strategy, and process conditions. To improve anti-blockingproperties, it is known to blend a VAE latex with a latex having betteranti-blocking properties, such as a vinyl acetate homopolymer or acryliclatex. Addition of fluorocarbon surfactants is also known to improveblock resistance by modifying surface properties. A fluorocarbonsurfactant acts as a surface-active agent that blooms to the top of afilm (the air interface) as it dries or cures and acts as a releaselayer that interferes with the intermingling of resin layers of twofilms in contact with one another. Additives of this class may beobtained from DuPont™ under the designation Capstone™ or Zonyl®, or 3M™under the designation Novec™, for example. See “DuPont™ Zonyl®Fluoroadditives as Antiblock Agents, A Comparative Study”, ProductLiterature, January 2003. See also, United States Patent Application2008/0145552 to Berrettini et al. which provides examples of suitablefluoroadditives. Fluorochemical additives may be added in an amount offrom about 0.05 weight % up to about 10 weight %. See also U.S. Pat. No.7,041,727 to Kubicek et al.

Wet adhesion refers to the ability of a latex paint to adhere to asubstrate under wet conditions. Wet adhesion is a critical property notonly for exterior paints, but also for some interior applications, suchas in kitchens and bathrooms.

Ethylene vinyl acetate binders (VAEs) are used primarily in interiorwith some exterior masonry applications. VAEs are characterized by lowT_(g) values, good touch-up in interior flat paints, and goodefflorescence resistance on masonry.

The paint of the invention comprises a resin that exhibits an improvedscrub performance of greater than 110% that of prior art and commercialpaints containing VAE resins. Without being bound to any theory, webelieve that the superior scrubbability of the present paint is due toincreased crosslink density in the resin, higher film strength, or moreuniform film formation.

Emulsion polymerization of ethylenically unsaturated monomers are wellknown as set forth in U.S. Pat. No. 5,874,498 to Daniels et al. and U.S.Pat. No. 6,028,139 to Farwaha et al., the disclosures of which areincorporated herein in their entirety. However, the resins of Daniels etal. are obviously more difficult and costly to make, since the molecularweight has to be carefully controlled.

The preparation of synthetic resin copolymer dispersions, where themonomers are copolymerized with hydrolysable, unsaturated organicsilicon compounds, is known. See, for example, U.S. Pat. No. 6,087,437to Farwaha, et al., U.S. Pat. No. 6,028,139 to Farwaha, et al. and U.S.Pat. No. 6,174,960 to Phan et al. Synthetic resin dispersions based onvinyl acetate with 0.5 to 1% by weight, based on the total amount ofmonomers, of a copolymerizable silane, such as, for example,vinyltrimethoxysilane, w-methacryloxypropyltrimethoxysilane and vinyltris(2-methoxyethoxy)silane, are also known from U.S. Pat. No. 3,729,438to Plesich et al. The polymer crosslinks on drying, giving rise to aclear, high-gloss film. Further, U.S. Pat. No. 3,814,716 to Kowalski etal. describes synthetic resin dispersions based on vinyl acetate,acrylic esters, maleic and fumaric esters with 0.5 to 5% by weight of acopolymerizable silane. On drying the synthetic resin dispersion yieldsclear, high-gloss and crosslinked films with excellent water and solventresistance. In addition, the use of polymeric binders in aqueousdispersion for the preparation of structural coating materials are knownfrom DE-PS 2,148,457, where the synthetic resin dispersions containpolymers from vinyl esters, acrylic esters or butadienestyrenecopolymers into which the silanol groups have been introduced bypolymerization. Furthermore, the preparation of aqueous synthetic resindispersions based on vinyl esters of carboxylic acids of 2 to 18 carbonatoms, ethylene, optionally up to 25% by weight of other olefinicallyunsaturated monomers and 0.3 to 5% by weight, based on the total amountof monomers, of an unsaturated hydrolysable organic silicon compound, isknown from DE-PS 2,148,458. Films prepared from the synthetic resindispersions described with copolymers containing 1 to 2% by weight ofthe silicon compounds named above, exhibit high drying and wet peelingstrengths on glass and asbestos cement. However, the synthetic resindispersion prepared according to Example 1 of the above DE-PS possessesa 0.2% by weight content of unreacted monomeric vinyl acetate and thesynthetic resin dispersions prepared according to Examples 6 and 10contain, respectively, 3.8 and 4.8% by weight of methanol, in each casebased on the polymeric part.

The use of other crosslinking monomers in the preparation of syntheticresin copolymer dispersions is similarly known, as disclosed in U.S.Pat. No. 6,624,243 to Stark et al. Such monomers may include epoxycontaining monomers: for example, monomers selected from the groupconsisting of glycidyl acrylate, glycidyl methacrylate, allyl glycidylether, vinyl glycidyl ether, vinylcyclohexene oxide, limonene oxide,myrcene oxide, caryophyllene oxide, vinyltoluenes and styrenessubstituted with a glycidyl radical in the aromatic moiety, andvinylbenzoates substituted with a glycidyl radical in the aromaticmoiety. Preferably, the monomers are selected from glycidyl methacrylateand allyl glycidyl ether. Such monomers may also include polymerizable1,3-dicarbonyl compounds: for example, acetoacetoxyethyl acrylate,acetoacetoxypropyl methacrylate, acetoacetoxyethyl methacrylate,acetoacetoxybutyl methacrylate, 2,3-di (acetoacetoxy)propylmethacrylate, and allyl acetoacetate. The amount of 1,3-dicarbonylcompound may range from 0.01 to 2% by weight, for example from 0.1 to 1%by weight, based in each case on the overall weight of the monomersused. Preferably, the monomers are selected from acetoacetoxypropylmethacrylate, acetoacetoxyethyl methacrylate, acetoacetoxybutylmethacrylate, 2,3-di (acetoacetoxy)propyl methacrylate and allylacetoacetate.

A variety of comonomers, e.g., ethylenically unsaturated monomers, canbe copolymerized with the vinyl acetate and ethylene. Any person skilledin the art knows on the basis of the T_(g) of the polymers and thepolymerization parameters which monomers or mixtures of monomers must beemployed to achieve resins of the parameters applied in this invention.The main monomers are optionally copolymerized with small amounts ofolefinically unsaturated silicon compounds containing hydrolysablegroups, for instance, silanes. The sum of the percentages of themonomers employed to form the copolymer is always 100.

Suitable sterically hindered alkoxylated silane monomers are disclosedin U.S. Pat. No. 6,174,960 to Phan et al., and are vinyltriisopropoxysilane, vinylpropyltriisopropoxy silane, vinylpropyltriisobutoxy silane,vinyltriisobutoxy silane, vinylpentyltri-t-butoxy silane,vinylpropylmethyldipentoxy silane, and vinylpropyltri-sec-butoxysilane.The sterically hindered alkoxylated silane monomer is preferablyvinyltriisopropoxysilane. The disclosure of '960 to Phan et al. isincorporated herein by reference in its entirety.

Blends of hard and soft emulsion polymers are known in the art. Blendingprovides a cost-effective solution to boost the performance of VAE-basedpaints. EP 466,409 A1 describes a system which contains a mixture of ahard latex with T_(g) greater than 20° C., and a soft latex with a T_(g)less than 15° C. The blend system described in EP 466,409 A1 isdisclosed to result in films with adequate film formation and hardnesswithout the use of a coalescent. U.S. Pat. No. 5,308,890 to Snyderdescribes a blend of emulsion polymers containing a soft stage polymerhaving a T_(g) of less than 50° C. and a hard stage polymer having aT_(g) of from 20° C. to 160° C., wherein the T_(g) of the soft stagepolymer is lower than the T_(g) of the hard stage polymer, and the hardstage polymer does not form a film at ambient temperature. U.S. Pat. No.3,935,151 to Nickerson, et al. describes an approach to improving thewet adhesion properties of vinyl acetate polymers by blending into avinyl acetate terpolymer, a copolymer which is a vinyl-acrylic, a vinylchloride-acrylic or an all-acrylic latex containing hydroxy methyldiacetone acrylamide (HMDAA). Similarly, U.S. Pat. No. 5,208,285 toBoyce, et al. describes providing improved wet-adhesion properties tovinyl acetate copolymers by blending into the vinyl acetate polymeremulsion, a minor amount of an all-acrylic emulsion or other emulsionshaving copolymerized therein a small quantity of a cyclic ureido monomerhaving wet adhesion-imparting properties, and the disclosure thereof isincorporated herein in its entirety. Hybrid polymer compositionscombining VAE with emulsified epoxy resin and isophoronediaminehardening agent have also demonstrated improved wet adhesion. Becausemany formulation variables affect cohesive strength, and therefore scrubresistance, blending can drastically change the film morphology andlatex/pigment interaction and, ultimately, film strength. As a result,latex characteristics may not be proportional to the blend ratio.

Two types of emulsions commonly used in formulating latex paints includethe all acrylic system, e.g., the systems employing copolymerized methylmethacrylate, butyl acrylate, or 2-ethylhexylacrylate with smallproportions of acrylic acid, etc., as may be desired, and vinyl acetateformulations usually in combination with a small proportion of the abovelower alkyl acrylates, e.g., butyl acrylate. Heretofore, the all acrylicsystem has been used in premium quality paints as the emulsions haveprovided for good water resistance, desired leveling, film hardness,durability, scrubbability, etc. The vinyl acetate-acrylic copolymersystems have been utilized in formulating interior flat and semi-glosspaints and exterior house paints. The vinyl acetate-butyl acrylatelatices when used in paint formulations result in paint films which haveexcellent toughness, scrub resistance and durability, while the vinylacetate-dibutyl maleate emulsions impart good abrasion resistance andflexibility as well as durability.

The paint formulations of the present invention may be prepared from ablend of aqueous emulsion polymers which are curable to form a film. Theblend may contain an ethylene-vinyl acetate (VAE) polymer and an acrylicor vinyl acrylic (i.e., vinyl acetate/butyl acrylate) polymer. Suchblends are desirable for achieving high performance characteristics,such as hardness, anti-blocking, and/or hi-gloss, in the paintformulation. The proportions of the respective polymers usually arebalanced to provide desired properties in the paint formulation, as iswell known in the art of latex paint.

The acrylic or vinyl acrylic polymer is present in an acrylic modifiedethylene-vinyl acetate polymer blend in an amount of from about 15 toabout 50 weight percent, preferably from about 20 to about 30 weightpercent, based on the total weight of the acrylic polymer and theethylene-vinyl acetate polymer. The ethylene-vinyl acetate polymer ispresent in an amount of from about 50 to about 85 weight percent,preferably from about 70 to 80 weight percent, based on the total weightof the acrylic polymer and the ethylene-vinyl acetate polymer.

Suitable acrylic unsaturated functional monomers commonly used toproduce all-acrylic emulsions include esters of methacrylic acid,including methyl methacrylate and butyl methacrylate, and esters ofacrylic acid, including ethyl acrylate, butyl acrylate and 2-ethylhexylacrylate. Specific examples of acrylate monomers include methylacrylate, ethyl acrylate, butyl acrylate, 2-ethyl hexyl acrylate, decylacrylate, methyl methacrylate, butyl methacrylate, iso-butylmethacrylate, iso-bornyl methacrylate hydroxy ethyl acrylate and hydroxyethyl methacrylate. Alternatively, the acrylic polymer may comprise astyrene acrylic latex.

While not being bound by any particular theory, the present inventorsbelieve that crosslinking occurs between the sterically hinderedalkoxysilane functionality on the acrylic polymer by means of ahydrolysis reaction to give silanols with subsequent condensationreaction between silanols and/or carboxyl groups on the acrylic polymer.Such crosslinking occurs during film formation of the coatingcomposition, most probably after particle coalescence or drying of thecoating composition. The advantage of preparing the coating compositionwith sterically hindered alkoxylated silane monomers is thatcrosslinking during the emulsion polymerization of the acrylic polymerand storage of the acrylic modified ethylene-vinyl acetate polymerblend, especially in the presence of carboxyl groups, is minimized.

The new resins having the components described herein may be obtainedfrom Celanese™ Emulsion Polymers under the designation EcoVAE® 405Series or by simply requesting high-scrub VAE resin, or by requestingsuitable resins using like terminology.

The paints are formulated using techniques known to those skilled in theart of manufacturing paint. Generally, water, defoamer, pigment, filler(also known as extender pigment) and surfactant stabilizer (in additionto emulsifiers used during emulsion polymerization) are combined to formthe grind, where the pigments and fillers are ground to a desiredparticle size as indicated by a Hegman reading of 2 to 6. The mostcommon way dispersion is checked is using a “Hegman.” Hegman numbersrelate to dispersion measured in microns. A higher Hegman number meansfiner grind. A Hegman number of about 2 to about 3 is almost exclusiveto a flat paint. Satin and Eggshell paints can have Hegman numbers inthe range of about 3 to about 6 depending upon formulation, preferablyin the range of 3 to less than 5. A Hegman number of about 6 representsa lower semi-gloss range. Additional water, latex binder, rheologymodifiers, biocides and the like are added to the grind and the entirebatch is blended and adjusted to desired Hegman readings and viscosity.

Preferred fillers used are, for example, calcium carbonate, magnesite,dolomite, kaolin, mica, talc, silica, calcium sulfate, feldspar, bariumsulfate and opaque polymer.

Examples of white pigments used are zinc oxide, zinc sulfide, basic leadcarbonate, antimony trioxide, lithopone (zinc sulfide+barium sulfate)and, preferably, titanium dioxide.

Examples of inorganic colored pigments which may preferably be used areiron oxides, carbon black, graphite, luminescent pigments, zinc yellow,zinc green, Paris blue, ultramarine, manganese black, antimony black,manganese violet or Schweinfurt green.

Suitable organic colored pigments preferably are, for example, sepia,gamboge, Cassel brown, toluidine red, para red, Hansa yellow, indigo,azo dyes, anthraquinone and indigo dyes as well as dioxazine,quinacridone, phthalocyanin, isoindolinone and metal complex pigments ofthe azomethine series.

The fillers may be used as individual components. Mixtures of fillerssuch as, for example, calcium carbonate/kaolin and calciumcarbonate/kaolin/talc have been found to be particularly useful inpractice. To increase the hiding power and to save on titanium dioxide,finely divided fillers such as, for example, finely divided calciumcarbonate and mixtures of various calcium carbonates with differentparticle size distribution are frequently used. Calcined clays arecommonly used to increase dry opacity as they help incorporate air voidsinto the dry film. Air voids create a big difference in refractive indexin the film and scatter light, yielding more opacity in the film oncecured.

To adjust the hiding power, the shade and the depth of color the fillersare mixed with appropriate amounts of white pigment and inorganic and/ororganic colored pigments.

To disperse the fillers and pigments in water, 0.1 to 0.6% by weight,based on the total weight of the aqueous preparation, of auxiliariesbased on anionic or non-ionic wetting agents, such as preferably, forexample, sodium pyrophosphate, sodium polyphosphate,naphthalenesulfonate, sodium polyacrylate, sodium polymaleinates andpolyphosphonates such as sodium 1-hydroxyethane-1,1-diphosphonate andsodium nitrilotris(methylenephosphonate), may be added.

Thickeners which may be used are, inter alia, preferably cellulosederivates such as methylcellulose (MC), hydroxyethylcellulose (HEC) andcarboxymethyl-cellulose. Other thickeners which may be used are casein,gum arabic, gum tragacanth, starch, sodium alginate, polyvinyl alcohol,polyvinylpyrrolidone, sodium polyacrylate and water-soluble copolymersbased on acrylic and methacrylic acid, such as acrylic acid/acrylamideand methacrylic acid/acrylic ester copolymers. Hydrophobically-modifiedalkali soluble (acrylic) emulsions (HASE), hydrophobically-modifiedethoxylate (poly)urethanes (HEUR), and polyether polyols (PEPO) are alsoavailable.

Inorganic thickeners, such as, for example, bentonites or hectorite, mayalso be used.

Such thickeners are generally employed in amounts from 0.1 to 3% byweight, preferably 0.1 to 1% by weight, based on the total weight of theaqueous preparations.

The thickener may be incorporated already during the dispersion of thefillers and pigments in water with the addition of a dispersant and, ifdesired, an antifoam, for example using a dissolver; however, thethickener may also be added to the finished preparation, provided thatthe water balance of the finished construction protective materialpermits this to be done.

The synthetic resin copolymer dispersion used as binder according to theinvention may already be present during the dispersion of the pigmentand filler, but in most cases it is advantageously added to thefiller/pigment paste which is still hot or also cooled, under rapid oralso slower stirring. In order to maintain a pigment volumeconcentration of 25% and above, 4 to 35 parts by weight of syntheticresin dispersion copolymer are used per 65 to 95.9 parts by weight offiller+pigment.

One feature that affects the overall combination of properties in alatex paint formulation is the particle size range present in theemulsion. When the proportion of large particles is high, scrubresistance of the resulting paint is reduced. When the proportion offines, i.e., those particles having a size less than 0.2 microns, ishigh, the paint will have poor flow and leveling characteristics. Theparticle size of latex in the polymer emulsion can be affected byadjusting the level of protective colloid or surfactant concentrationadded initially or incrementally during polymerization. Agitation isanother variable which can affect particle size in the polymer emulsion.These factors may be adjusted as necessary by methods known in the art.

For various applications, it is sometimes desirable to include smallamounts of additives, such as bactericides, pH modifiers, andantifoamers, incorporated in the latex. This may be done in aconventional manner and at any convenient point in the preparation ofthe latexes.

A feature according to the invention is that the paint formulationsaccording to the invention are free from readily volatile residualmonomers, from low alcohols and from ammonia and/or volatile amines orfrom components which give rise by cleavage to H₂S or mercaptans, ifappropriate, and the total volatile organic content of the paintformulations is <0.1% by weight, based on the total non-volatile part.

Furthermore, the preparations according to the current invention arefree of alkyl phenol ethoxylates (APE) and octyl phenol ethoxylates, aclass of compounds typically used as surfactants that degrade tophenols; i.e., the paint formulation of the current invention isAPE-free. These compounds are of environmental concern due to theirestrogen mimicking characteristics.

Accordingly, the subject matter of the invention are low-emission,high-scrub VAE latex dispersion paint formulations in the form ofaqueous preparations based on aqueous synthetic resin dispersionpolymers of the class disclosed in U.S. Pat. No. 5,576,384 to Nolken, etal., the disclosure of which is incorporated herein by reference. Thepaints of this invention have a pigment volume concentration (PVC) offrom about 25 to about 85 weight %; and contain water, fillers,pigments, synthetic resin dispersion polymers, and auxiliaries selectedfrom the group consisting of wetting agents, dispersants, emulsifiers,protective colloids, thickeners, antifoams, dyes, pH adjusters/buffers,non-APE non-ionic surfactants, and preservatives. The non-volatile partof the paint formulation contains

-   -   10 to 94% by weight of a filler,    -   2 to 30% by weight of a pigment,    -   0.1 to 10% by weight of an auxiliary and    -   2 to 40% by weight of a synthetic resin dispersion copolymer,        based on the total non-volatile part. The dispersion copolymer        possesses a K-value greater than 60 coupled with a gel content        greater than 50% and the synthetic resin dispersion copolymer        preferably has a content of monomeric units derived from        unsaturated hydrolysable organic silicon compounds. In        particular, the synthetic resin dispersion copolymer preferably        incorporates from 0.1 to 5 weight % of the residue of a silane        monomer. More preferably, 0.1 to 0.5 weight % of the residue of        a silane monomer is incorporated.

If appropriate, the following components may be added as auxiliaries inaddition to the constituents from the synthetic resin copolymerdispersion:

-   -   0.1 to 0.6% by weight of a wetting agent or dispersant for        filler and pigment,    -   0.1 to 1% by weight of a thickener,    -   0.01 to 2% by weight of a preservative and    -   0.001 to 0.5% by weight of an anti-foam,        each based on the total weight of the aqueous preparations.

Commercially available pigment pastes may be used to tint dispersionpaints, or pigment may be admixed with the synthetic resin dispersion orthe white dispersion paint or the dispersion plaster in the dry state,if desired.

Alkali metal salts may be used instead of ammonium salts and amine saltsin preparing the copolymer dispersion to avoid undesirable odors andvolatilized amine emissions.

Synthetic resin copolymer dispersions based on vinyl acetate/ethyleneare preferably used for the odorless aqueous preparations, low innoxious substances emission, of construction protective materials, inaddition to water, filler, pigment, dispersant, thickener, antifoam, andpreservative.

The above dispersion copolymers based on vinyl acetate/ethylene and withcomonomers of the silane class are particularly preferred according tothe invention.

When these dispersion copolymers are used as binders in the paintformulations under discussion, the so-called crazing of the driedcoating and of the dried coating even after only a brief drying periodof the preparation, as assessed by the resistance to washing andshearing of coatings according to DIN 53,778, does not occur, despitethe absence of solvents and film-consolidating auxiliaries, i.e., thecoating possesses mechanical strength after a brief drying period, ascan be frequently observed with paints derived from polymer dispersions.

Those aqueous preparations of construction protective materialsaccording to the invention are particularly suitable and preferred whichcontain solvent-free synthetic resin copolymer dispersions as bindersand whose copolymers contain monomeric units derived from siliconcompounds, which units are capable of copolymerization and carryhydrolysable silicon-containing radicals or form Si(OH)_(x) groups (x=1to 3), and the copolymers were prepared by emulsion copolymerizationfrom combinations of comonomers which result in the required values, inthe presence of a thickener, a non-ionic emulsifier, and small amountsof monomeric sulfur compounds.

It is believed that a branched polymer architecture in the copolymerexhibits a higher tensile storage modulus at elevated temperatures. Onecan generate a range of aqueous copolymer dispersions containing a rangeof T_(g) and a high tensile storage modulus at high temperatures; i.e.,temperatures of about 115° C. The tensile storage modulus profile forthese polymers provides an insight to the distribution of vinyl acetateand ethylene in the polymer and the melt flow characteristics. They havespecific viscoelastic properties as indicated by tensile storage modulusof the cast film.

It cannot be simply assumed or deduced from the above state of the artthat synthetic resin dispersions with or without silanol groups may alsogive rise to an improvement of the scrubbability of the coatingsproduced by the paints.

Typical characteristics of a resin used in a paint formulation accordingto the invention are described below.

TABLE 1 VAE Resin Characteristics Stabilizing system Emulsifier Solidcontent 55% Viscosity 50-1000 cps Average particle size 200 nm T_(g) 13°C. MFFT  0° C. pH 4.5-6 Film on glass Clear

Comparative approximate characteristics of EcoVAE® 405 Series laticesused in a paint formulation according to the invention in relation toCelvolit® 1774 and a high molecular-weight commercial latex aredescribed in Table 2, below.

TABLE 2 Comparative Resin Characteristics Solids, Viscosity, MFFT, VAM,Sample % cps pH T_(g) ° C. ppm Celvolit ® 55.7 294 5.2 10.0 0 900 1774EcoVAE ® 55.8 396 5.3 9.6 0 600 Series 405 Latex A EcoVAE ® 55.2-56.1262-510 5.3 10.0-10.8 0 close Series 405 to 500 Latex B

Ingredients and procedure for preparing a paint formulation according tothe invention are described as in Tables 3 and 4, below. Characteristicsof the inventive paint formulation comprising a resin as described aboveare also listed below, first for a flat paint, and subsequently for aneggshell paint.

TABLE 3 Flat (51 PVC) Ingredient Amount (lbs) Water 208.00 EthyleneGlycol (cosolvent) 18.50 Nuosept ® 498 (preservative) 0.75 Carbowet 100(surfactant) 4.00 Drewplus T-4507 (defoamer) 0.50 Natrosol Plus 330(thickener) 2.00 Mix, then add: AMP 95 (pH adjuster/buffer) 2.00Nuosperse FX605 L (dispersing agent) 7.50 Kelzan S(suspending/thickening/dispersing agent) 0.50 Diafil 525 (extenderpigment) 40.00 Huber 70C (extender pigment) 90.00 Camelwite (extenderpigment) 145.00 Kronos 2310 (pigment) 180.00 Disperse to 2-3 HegmanWater 125.00 Cognis DSX 3800 (thickener) 10.50 VAE resin 307.50 DrewplusT-4507 (defoamer) 4.00 Water 22.00 Total 1167.75 Viscosity 95-100 KrebUnits (KU) pH 8.8-9.2 Weight per Gallon 11.6 ± 0.1 pounds per gallon 60°Gloss 1-3 85° Sheen 1-3 Dry to Touch 2 hours VOC <60 G/L

TABLE 4 35 PVC Eggshell Ingredient Amount (lbs) Water 250.0 PropyleneGlycol (cosolvent) 10.0 Natrosol Plus 330 (thickener) 2.2 AMP-95 (pHadjuster/buffer) 3.0 Acticide BW-20 (preservative) 1.1 Cognis A-38Defoamer 2.5 Tamol 1124 Dispersant 3.6 Carbowet 106 (surfactant) 3.0Mix, then add: Tronox CR-826 (pigment) 200.0 Minex 7 (extender pigment)50.0 Optiwhite (extender pigment) 75.0 Water 73.5 Disperse to 5.0-6.0Hegman Letdown: VAE resin 375.0 Texanol (cosolvent) 10.0 RM-825(thickener) 14.0 Cognis A-38 Defoamer 2.5 Water 11.7 Total 1075.4 PVC35% Volume Solids 35% VOC <100 g/L Viscosity 95-100 KU ICI¹ 1.0-1.1 pH8.5-9.5 Weight per Gallon 10.8 ± 0.1 pounds per gallon 60° Gloss 4.0-5.085° Sheen  9.0-10.0 Contrast Ratio 96.8 Y Reflectance 91.3 ¹ImperialChemical Industries (ICI) number refers to a rheological instrumentwhich is used to measure high shear viscosity. A higher ICI numberindicates a thicker coating would adhere to the substrate.

Materials Description and Source

NUOSEPT™ 498 is a 1,2-benzisothiazolin-3-one preservative, availablefrom International Specialty Products.

CARBOWET® 100 is a surfactant for pigment and substrate wetting,available from Air Products.

DREWPLUS® T-4507 is a foam control agent, available from Ashland WaterTechnologies, Drew Industrial.

NATROSOL® PLUS 330 is a hydroxyethyl cellulose thickener, available fromAqualon™, a business unit of Hercules™.

AMP-95® is a 2-amino-2-methyl-1-propanol pH adjuster/buffer, availablefrom ANGUS Chemical Company.

NUOSPERSE® FX 605 L is a dispersant, available from Elementis™Specialties, Inc.

Kelzan® S is a xanthan gum suspending/thickening/dispersing agent,available from CP Kelco™.

DIAFIL® 525 is diatomaceous earth filler, available from WorldMinerals™.

HUBER® 70C Calcined Kaolin Clay is a filler, available from Huber™Engineered Materials.

Camelwite is a calcium carbonate filler, available from Imerys™/CR WorldMinerals.

Kronos™ 2310 is a titanium dioxide pigment, available from Kronos™.

DSX® 3800 is a thickener, available from Cognis-Polymers, Coatings andInks.

ACTICIDE® BW 10/BW 20 is an aqueous-based benzisothiazolinonepreservative, available from Thor Specialties, Inc.

FoamStar A-38 is a dispersible modified defoamer, available fromCognis-Polymers, Coatings and Inks.

Tamol® 1124 is a dispersant, available from Rohm and Haas™ Company.

CARBOWET® 106 is an alcohol ethoxylate surfactant, available from AirProducts™—Additives.

TRONOX™ CR-826 is a silica/alumina-treated rutile pigment, availablefrom Tronox™, Inc.

Minex™ 7 is a nepheline syenite extender pigment, available from Unimin™Specialty Minerals, Inc.

OPTIWHITE P® is a calcined aluminum silicate extender pigment, availablefrom Burgess Pigment.

TEXANOL™ ester alcohol is a coalescent, available from Eastman™ CoatingsFilm Technologies.

ACRYSOL™ RM-825 is a hydrophobically modified polyethylene oxideurethane thickener, available from Rohm and Haas™ Company.

EcoVAE™ 405 Series is a high-scrub, low residual monomer, low-odor vinylacetate/ethylene (VAE) emulsion, available from Celanese™ (EmulsionPolymers), Houston, Tex., which may be obtained by simply requestinghigh-scrub VAE resin or requesting suitable resins using liketerminology.

The invention is elucidated in greater detail by the examples below. Inthe Examples, parts and percentages are by weight. In the examplesbelow, the high molecular weight commercial latex provides a resin ofthe class disclosed in U.S. Pat. No. 5,874,498 to Daniels et al., andthe Celvolit® 1774 example provides a resin of the class disclosed inU.S. Pat. No. 5,576,384 to Nolken et al. EcoVAE® 405 Series Latex A is anewly available resin that does not contain silane. EcoVAE® 405 SeriesLatex B is a newly available resin that contains silane in the polymerstructure.

The following test procedures and organic-solvent-free, latex paintformulations were used to evaluate the latex binders and latex paints ofthe present invention.

ASTM D4946 is used to evaluate blocking of a paint formulation. TheBlocking Resistance Method Standard Operating Procedure is as follows.

Materials Required

-   -   1. (6″) 6 mil Clearance Bird Bar    -   2. Vacuum Plate    -   3. Sealed Test Chart    -   4. Paint Sample    -   5. Paper Cutter    -   6. 1 kg weight    -   7. 50° C. Oven    -   8. Stopwatch or Timer

Procedure

Preparation of Drawdown

-   -   1. Turn on vacuum pump.    -   2. Center test chart on vacuum plate and label appropriately.    -   3. Ensure paint sample is homogenous (stir first).    -   4. Place a clean, 6 mil drawdown bar below labeled portion of        chart.    -   5. Dab sufficient paint near the edge of the blade to form a        continuous film the length of the panel.    -   6. Draw 6 mil bar slowly and evenly to the length of the chart.    -   7. Clean and dry the bar immediately.    -   8. Remove the chart to a horizontal surface.        -   Repeat procedure for each sample.

Preparation of Test Samples

The block test may be performed once the cards have conditioned aminimum of (16) sixteen hours.

-   -   1. Using a paper cutter, cut fully paint covered squares 1.5        ″(4 cm) wide. Four squares are required for each period of        testing.    -   2. Pair the squares face-to-face and label each with the        appropriate information (Sx ID, Oven (OV), or ambient (RT)).    -   3. Place one pair of squares in constant temperature room on a        continuous flat surface/benchtop.    -   4. Center one #8 rubber stopper (narrow end down) and place        weight totaling 1000 g on square.    -   5. Remove stopper and weight from this pair of squares the next        day.    -   6. Place the second pair in the 50° C. oven and repeat step 4.    -   7. After 30 minutes remove pair from oven to cool.

Evaluation of Test Samples

Evaluation of samples may be required after the panels have dried 24hours, 48 hours, 72 hours, 4 days, 5 days, or 7 days. Record theresults.

-   -   1. Pull the squares apart, listening for sounds tack and looking        for signs of film damage or rupture.    -   2. Rate squares according to the given numerical ratings per        Table 5.

TABLE 5 Rating of Block Resistance Samples Rating Description 10 No tack9 Trace tack 8 Very slight tack 7 Very slight to slight tack 6 Slighttack 5 Moderate tack 4 Very tacky 3 Film ruptures 5-25% 2 Film ruptures25-50% 1 Film ruptures 50-75% 0 Film ruptures 75-100%

The dye stain test is a porosity test used by the paint industry to lookat film porosity/sealing of the paint surface for flat through eggshellfinishes. The test is conducted as follows:

-   -   1) Make a 1% solution by weight of water-dispersible Nigrosin        dye.    -   2) Make a 3 mil wet draw down side-by-side on a Leneta card and        cure overnight.    -   3) Using a 1-2″ foam brush, apply a liberal amount of the 1% dye        stain solution across the card and allow to sit for 1 minute.    -   4) Take a damp sponge and wipe off the excess dye after 1        minute. Wipe a total of three times, using a clean surface on        the sponge each time.    -   5) Allow to dry.

Results may be rated visually, or the change in L* value compared to thewhite paint for the stained section may be measured. See FIG. 4.

The Fikentscher K value range (H. Fikentscher, Cellulosechemie 13(1932), 58-64 and 71-74) is a measure of intrinsic viscosity analogousto DIN 53726, and indicative of the molecular weight of a polymer. Asthe K value increases, the strength and scrubbability correspondinglyincrease. To determine the K value, dissolve an equivalent of 1 g of drypolymer (=2 g of a 50% solids containing dispersion) in 100 ml dimethylformamide (DMF) at room temperature while stirring (until completelydissolved, at least 1 h), and determine the viscosity of the solution at23° C., using a Mikro-Ostwald-Viscometer (Capillary type 518 13/I c [2ml]; Schott AVS 400+CT1150). Then determine the viscosity of 1 g ofwater in 100 ml DMF at 23° C. in the same viscometer. Insert theviscosity readings and the polymer concentrations into equation A andcalculate the k value. The K value is obtained by multiplying the kvalue by 1000.

log=η_(c)/η_(o)[(75*k ²)/(1+1.5k*c)+k]*c  (A)

Scrub resistance was tested as follows. A test scrub panel was preparedby drawing a 7.0 mil film of paint on a Leneta chart and allowing thepaint to dry for 7 days in an open room maintained at 23±2° C. and 50±5%relative humidity. The dried chart was affixed to a glass panel and putinto a scrub machine equipped with a scrub brush and a basin for holdingthe text panel. The brush was prepared by immersing it overnight inwater. The brush was placed in the machine holder and the test scrubpanel was put under the brush. The brush bristles were spread evenlywith 10 grams of a standardized scrub medium (available fromBYK-Gardner). The panel was then wet with 5 ml of reagent water in thepath of the brush. The scrub machine was started. After every 400strokes before failure, 10 grams of scrub medium and 5 ml of reagentwater were added to the brush bristles. The number of strokes to thepaint at which 0.5 inch of black chart shows through the test panel wasrecorded. Table 6 provides test results for paint formulationscontaining various resins. The paint formulations have approximately thescrub values shown below. The Relative Scrub Index of a latex isexpressed in percent relative to Celvolit® 1774 latex (being a value of100%) in a 51 PVC formulation as described hereinafter. Celvolit® 1774characteristics are provided in Table 2, above.

TABLE 6 K-value and Scrub Results Ratio of Scrub Relative Scrub Relativecycles, Index, ½″ Scrub ½″ Scrub Scrub in 51 Index in 51 PVC vs. to K-K-Value PVC Celvolit ® 1774 value Celvolit ® 1774 48.6  596 100% 2.06High 94 1133-1492 192% 2.04 molecular- weight commercial latex EcoVAE ®405 83.6 1349 229% 2.74 Series Latex A EcoVAE ® 405 71.2-93.1  839-2184165-240% 2.32-2.58 Series Latex B

As can be seen in Table 6, K-values of the EcoVAE® 405 Series laticesexceed that of the Celvolit® 1774 and are in the range of that of thehigh molecular weight commercial latex. However, the EcoVAE® 405 Serieslatices may be used to produce a paint formulation that exhibits asurprisingly higher ratio of relative scrub index to K-value than eitherthe high molecular-weight commercial latex or the Celvolit® 1774.Without being bound by theory, improved scrubbability might beadditionally correlated with the combination of crosslink density,molecular weight, tensile strength and film toughness of the new EcoVAE®405 Series latices.

Tensile Storage Modulus

There is a correlation between K-values and G′ (storage modulus) values;samples with higher K-values show higher G′ values. Tensile storagemodulus as a function of temperature was measured at a test frequency of6.28 rad/sec and expressed as Pascals. More specifically, dynamicmechanical testing of the polymer samples for measuring shear storagemodulus may be measured using the following procedure. Each polymeremulsion was cast as a film and dried for four days at 23° C. and ahumidity between 50 and 60%. The dry film thickness was typically in therange between 0.4 and 0.7 μm. A round test specimen was cut with acircular cutter and a diameter of 25 mm. The specimens were tested on aMalvern™ CVO 120 rheometer with a plate-plate geometry with each 25 mmdiameter (measuring system ETC PP 25) to determine the shear storagemodulus G′ as a function of temperature. The test specimen wasintroduced in the system at room temperature. After heating to 130° C.and 420 s compensation time the measurement was started. Data wereobtained over a range from 130 to 0° C. with a cooling rate of 2 K/minand a frequency of 6.28 rad/s. The deformation was 0.064 with an initialstress of 1000 Pa. Due to a different gap in between the two plates,depending on the temperature the gap was adjusted automatically in a waythat a force of 100 N was always applied on the sample. For eachtemperature the CVO 120 calculated the shear storage modulus (G′) basedon the diameter and thickness of the sample. See FIG. 5.

When determining K-value, it is assumed that the sample fully dissolvesin the solvent. If there are minute gels, the fraction which is notdissolved would not contribute to the K-value. Therefore, gel contentwas determined as described below.

Determination of Gel Content (Cured Samples)

1) Sample Preparation:

30 g of dispersion (containing 53-55% solids) were diluted with 20 g ofdemineralized water, and 2 drops of Agitan® 282 (defoamer) were added.The mixture was carefully stirred for 15 minutes at room temperatureusing a magnetic stirrer bar. The mixture was poured onto a Teflon®plate (diameter: 17.8 cm, height 4 mm). After drying for 72 hours at 25°C. and 50% humidity, the film was turned and dried under the sameconditions for an additional 24 hours. The films were cured for 14 hoursat 125° C.

2) Determination of Gel Content

2.00 g (W₀) of polymer film were weighed into centrifuge tubes, 15 ml oftetrahydrofuran (THF) were added, and the samples were capped and shakenfor 40 hours. The tubes were centrifuged (30 minutes @ 15,000 rpm) andthe transparent layer was poured out. The remaining sample (presumed tobe the gel) was dried and weighed (W₁). The gel content [%] wascalculated from the following expression:

Gel content [%]=(W ₁ /W ₀)*100

TABLE 7 Gel Content of Cured Resin Samples Weight Gel contentDescription (dried gel) [g] [%] Celvolit ® 1774 1.98 99.0% Highmolecular weight commercial latex 0.69 34.5% EcoVAE ® 405 Series Latex A0.17 8.5% EcoVAE ® 405 Series Latex B 1.92-2.00 96-100%

The cured EcoVAE® Latex A exhibits a lower gel content than any of otherthe samples disclosed in Table 7.

Determination of Gel Content (Uncured Samples)

1) Sample Preparation:

30 g of dispersion (containing 53-55% solids) were diluted with 20 g ofdemineralized water, and 2 drops of Agitan® 282 (defoamer) were added.The mixture was carefully stirred for 15 minutes at room temperatureusing a magnetic stirrer bar. The mixture was poured onto a Teflon®plate (diameter: 17.8 cm, height 4 mm). After drying for 72 hours at 25°C. and 50% humidity, the film was turned and dried under the sameconditions for an additional 24 hours. The films were dried for anadditional 11 days (films were turned over daily).

2) Determination of Gel Content

2.00 g (W₀) of polymer film were weighed into centrifuge tubes, 15 ml ofTHF were added, and the samples were capped and shaken for 40 hours. Thetubes were centrifuged (30 min @ 15,000 rpm) and the transparent layerwas poured out. The remaining sample (presumed to be the gel) was driedand weighed (W₁). The gel content [%] was calculated from the followingexpression:

Gel content [%]=(W ₁ /W ₀)*100

TABLE 8 Gel Content of Uncured Resin Samples Gel Weight contentDescription Remarks (dried gel) [g] [%] Celvolit ® 1774 Solventcompletely 2.0 100 absorbed High molecular weight Viscous hazy 0 0commercial latex solution EcoVAE ® 405 Series Viscous hazy 0 0 Latex Asolution EcoVAE ® 405 Series Solvent completely 2.0 100 Latex B absorbed

As can be seen in Table 8, the uncured EcoVAE® 405 Series Latex Aexhibits a gel content comparable to the uncured high molecular weightcommercial latex, whereas the uncured EcoVAE® 405 Series Latex Bexhibits a gel content comparable to the uncured Celvolit® 1774.

Determination of Relative Swelling Ratio, S_(r)

1) Sample Preparation:

30 g of dispersion (containing 53-55% solids) were diluted with 20 g ofdemineralized water, and 2 drops of Agitan® 282 (defoamer) were added.The mixture was carefully stirred for 15 minutes at room temperatureusing a magnetic stirrer bar. The mixture was poured onto a Teflon®plate (diameter: 17.8 cm, height 4 mm). After drying for 72 hours at 25°C. and 50% humidity, the film was turned and dried under the sameconditions for an additional 24 hours.

The films were cured for (a) 7.5 minutes at 125° C., or (b) 14 hours at125° C.

Using a die cutter, round plates with a diameter of 1.5 cm wereprepared.

2) Determination of the S_(r)-Value

One sample each was mixed with 28 ml of solvent in a 100 ml beaker, andleft to soak for 3 hours. The contents were then poured onto a Petridish lying on a graph paper and the diameter was measured. The S _(r)-value was calculated as follows:

S _(r) =(diameter of swollen sample [cm])/1.5 cm

A) Curing for 7.5 minutes @ 125° C.

TABLE 9 Resin Swelling Results after 7.5 minutes curing @ 125° C.Diameter Diameter [cm]; [cm]; solvent: solvent: S_(r) THF S_(r) (THF)Acetone (Acetone) Thickness (sample 1/ (avg. of 2 (sample 1/ (avg. of 2Description [mm] sample 2) measurements) sample 2) measurements)Celvolit ® 0.40 +/− 0.02 dissolved — dissolved — 1774 High 0.55 +/− 0.02dissolved — dissolved — molecular weight commercial latex EcoVAE ® 0.53+/− 0.02 dissolved — dissolved — 405 Series Latex A EcoVAE ® 0.42 +/−0.02 4.2/4.4 Up to 2.9 4.1/4.2 Up to 2.8 405 Series Latex B

As shown in Table 9, only the EcoVAE® 405 Series Latex B exhibitedmeasureable swelling in either solvent. Without intending to be bound bytheory, the swelling exhibited by the EcoVAE® Series 405 resins isbelieved to be representative of trapped solvent. Results followingfurther curing and using other solvents are shown below.

B) Curing for 14 h @ 125° C.

TABLE 10 Resin Swelling Results in THF after 14 hours curing @ 125° C.Diam. [cm]; solvent: THF S_(r) (THF) Thickness (sample 1/ [avg. of 2Description [mm] sample 2) measurements] Celvolit ® 1774 0.40 +/− 0.024.6/4.8 3.1 High molecular 0.55 +/− 0.02 dissolved — weight commerciallatex EcoVAE ® 405 Series 0.53 +/− 0.02 dissolved — Latex A EcoVAE ® 405Series 0.37-0.59 +/− 4.3-5.3/4.3-5.3 2.9-3.5 Latex B 0.02

As shown in Table 10, above, the high molecular weight commercial latexand the EcoVAE® 405 Series Latex A both dissolved in THF. Swellingresults for the EcoVAE® 405 Series Latex B was slightly lower than thatof the Celvolit® 1774. No difference was noted when the resins weresoaked in n-Heptane.

TABLE 11 Resin Swelling Results in Acetone and i-Propanol after 14 hourscuring @ 125° C. Diam. [cm]; Diam. solvent: [cm]; Acetone S_(r) solvent:i- S_(r) (i- (sample 1/ (Acetone) Propanol Propanol) Thickness sample[avg. of 2 (sample 1/ [avg. of 2 Description [mm] 2) measurements]sample 2) measurements] Celvolit ® 0.40 +/− 0.02 4.4/4.7 3.03 1.5/1.5 11774 High 0.55 +/− 0.02 Dissolved — 1.5/1.5 1 molecular weightcommercial latex EcoVAE ® 0.53 +/− 0.02 Dissolved — 1.6/1.7 1.10 405Series Latex A EcoVAE ® 0.37-0.59 +/− 4.0-4.7/ 2.7-3.17 1.5-1.7/ 1-1.13405 Series 0.02 4.0-4.8 1.5-1.7 Latex B

As can be seen in Table 11, similar results were achieved when soakingthe resins in acetone as were discussed for soaking the resins in THF,although Celvolit® 1774 and the EcoVAE® 405 Series Latex B exhibitedslightly lower swelling in acetone than in THF. Similar results wereachieved when soaking the resins in i-propanol as were discussed forsoaking the resins in n-heptane, although both EcoVAE® 405 Serieslatices exhibited slightly higher swelling in i-propanol than wasexhibited in n-heptane. Refer to the discussion below Table 10, above.

TABLE 12 Resin Swelling Results in ethyl acetate after 14 hours curing @125° C. Diam. [cm]; solvent: ethyl S_(r) acetate (ethyl acetate)Thickness (sample 1/ [average of 2 Description [mm] sample 2)measurements] Celvolit ® 1774 0.40 +/− 0.02 4.5/4.6 3.03 High molecular0.55 +/− 0.02 Dissolved — weight commercial latex EcoVAE ® 405 Series0.53 +/− 0.02 Dissolved — Latex A EcoVAE ® 405 Series 0.37-0.59 +/−4.0-4.7/4.1-4.6 2.7-3.10 Latex B 0.02

As can be seen in Table 12, similar results were achieved by soaking theresins in ethyl acetate as were achieved by soaking the resins inacetone. Refer to Table 11, above.

Flat, eggshell, and semigloss paint formulations in accordance with theinvention have approximately the block resistance, scrub resistance, andstain resistance values shown below.

TABLE 13 Properties of Paint Formulations Using Various Resins (Flat)High molecular weight EcoVAE ® 405 Series Resin in 51 PVC FlatFormulation Celvolit ® 1774 commercial latex Latex B WPG 11.63 11.5711.61-11.68 Init. Viscosity (KU) 93 94 87-92 init. pH 9.48 9.439.50-9.60 Eq. Viscosity (KU) 97 95 89-96 Eq. pH 9.21 9.35 9.11-9.4  ICI(Poise) 0.963 0.833 0.883-1.296 Low temperature Coalescence Pass PassPass Wet Adhesion (3 mils - 1/3/7 days dry @ RT) n/a n/a n/a DryAdhesion (3 mils - 1/3/7 days dry @ RT) n/a n/a n/a Gloss (20°/60°/85°)(3 mils) 1 day dry @ RT 1.2/2.3/2.5 1.2/2.3/2.7 1.2/2.3/2.6-2.8 2 daysdry @ RT 1.2/2.3/2.5 1.2/2.3/2.7 1.2/2.3/2.5-2.7 3 days dry @ RT1.2/2.3/2.5 1.2/2.3/2.8 1.2/2.3/2.7 7 days dry @ RT 1.2/2.3/2.51.2/2.3/2.8 1.2/2.3/2.7 Brightness (3 mils - 24 hrs @ RT - white region)88.96 89.04 88.95 Contrast Ratio 96.71 96.48 95.77 Stain Resistance %removal (6 mils - 7 days dry @ RT) Hydrophilic stains Grape juice 2 22-5 Ketchup 85 95 95 Mustard 5 5 5 Coffee 5 5 5 Hydrophobic stainsLipstick 60 50 60-95 Marker 80 90 80-90 Pen 2 5 2-5 Pencil 80 80 80Crayon 5 5  5-10

TABLE 14 Properties of Paint Formulations Using Various Resins(Eggshell) High molecular weight Resin in 35 PVC Eggshell FormulationCelvolit ® 1774 commercial latex EcoVAE ® 405 Series Latex B WPG 10.8710.86 10.88-10.89 Init. Viscosity (KU) 95 89 79-91 init. pH 9.45 9.509.34-9.45 Eq. Viscosity (KU) 96 91 81-91 Eq. pH 9.07 9.20 9.07-9.21 ICI(Poise) 0.792 0.600 0.638-0.721 Flow & Levelling (LTB-2 blade, ASTMD4062) 5 5 5 Flow & Levelling (NYPC blade) 2 2 1-2 Sag Resistance(ASTM-4 blade) 17.6 15.6 13.6-17.6 Low temperature Coalescence Pass PassPass Gloss (20°/60°/85°) (3 mils) 1 day dry @ RT 1.3/3.8/8.4 1.3/3.8/7.91.3/3.7-4.1/8.8-9.4 2 days dry @ RT 1.3/3.7/8.0 1.3/3.8/7.71.3/3.6-3.9/8.4-9.0 3 days dry @ RT 1.3/3.6/7.8 1.3/3.7/7.31.3/3.5-3.9/8.1-8.5 7 days dry @ RT 1.3/3.6/7.7 1.3/3.6/7.1 1.3/3.8/7.9Brightness (3 mils - 24 hrs @ RT - white region) 90.94 91.07 91 ContrastRatio 96.41 96.65 96.36 Stain Resistance % removal (6 mils - 7 days dry@ RT) Hydrophilic stains Grape juice 10 5 5 Ketchup 95 95 95 Mustard 5 55 Coffee 10 5 5 Hydrophobic stains Lipstick 85 70 90-95 Marker 70 9080-90 Pen 5 5 2-5 Pencil 25 50 20-25 Crayon 85 95 90

TABLE 15 Properties of Paint Formulations Using Various Resins(Semigloss) High molecular weight Resin in 25 PVC Semigloss PaintFormulation Celvolit ® 1774 commercial latex EcoVAE ® 405 Series Latex BWPG 10.64 10.66 10.68 Init. Viscosity (KU) 90 84 78-88 init. pH 9.059.24 8.95-9.13 Eq. Viscosity (KU) 94 85 79-90 Eq. pH 8.68 8.91 8.72-8.85ICI (Poise) 0.738 0.663 0.738-1.192 Flow & Levelling (LTB-2 blade, ASTMD4062) 6 6 5-6 Flow & Levelling (NYPC blade) 3 3 2-3 Sag Resistance(ASM-4 blade) 17.6 13.6 15.6-17.6 Low temperature Coalescence Pass PassPass Gloss (20°/60°/85°) (3 mils) 1 day dry @ RT 11.2/52.2/92.922.3/64.0/92.3 7.5-13.1/41.9-54.0/84.7-91.5 2 days dry @ RT11.0/52.0/92.6 21.4/63.2/92.1 6.7-12.3/39.9-53.0/83.5-91.1 3 days dry @RT 9.9/50.0/92.2 21.3/63.0/91.5 6.2-12.0/38.6-52.4/83.3-90.3 7 days dry@ RT 9.0/48.6/91.2 20.4/62.4/91.5 11.1/51.0/89.4 Brightness (3 mils - 24hrs @ RT - white region) 91.95 92.43 91.85 Contrast Ratio 96.84 96.8396.91 Stain Resistance % removal (6 mils - 7 days dry @ RT) Hydrophilicstains Grape juice 5 5 5 Ketchup 95 95 95 Mustard 5 5 5 Coffee 5 5 5Hydrophobic stains Lipstick 95 95 95 Marker 10 70 50 Pen 5 10 50 Pencil2 5 5 Crayon 95 95 95

While the invention has been described in connection with severalembodiments, modifications of those embodiments within the spirit andscope of the present invention will be readily apparent to those ofskill in the art. The invention is defined in the appended claims.

What is claimed is:
 1. A water-based, low-emission latex paintformulation comprising: (a) a vinyl acetate/ethylene (VAE) latexincluding a VAE resin consisting of (i) from 80 to 95 weight % vinylacetate residue and (ii) from 5 to 20 weight % ethylene residue; (b) apigment composition including solids selected from the group consistingof inorganic pigments, inorganic fillers and mixtures thereof present inan amount such that the paint formulation has a pigment volumeconcentration (PVC) of from 25% to 85%; and (c) one or more auxiliarycomponents selected from the group consisting of wetting agents,dispersants, emulsifiers, protective colloids, thickeners, antifoams,dyes and preservatives; wherein (i) the resin has a K-value of greaterthan 60, (ii) the paint formulation exhibits a relative scrub index ofgreater than 200% and up to 300%, and (iii) the ratio of the relativescrub index of the latex to the K-value of the resin is at least 2.25/1;and wherein the resin and the paint formulation are alkylphenolethoxylate (APE)-free.
 2. The water-based, low-emission paintformulation according to claim 1, wherein the ethylene residue in theresin is from 10 to 15 weight %.
 3. The water-based, low-emission paintformulation according to claim 1, wherein the paint formulation has avolatile organic content less than 5 g/L.
 4. The water-based, lowemission paint formulation according to claim 1, wherein the paintformulation further comprises a block-resistant additive.
 5. Awater-based, low-emission latex paint formulation comprising: (a) avinyl acetate/ethylene (VAE) latex including a VAE resin with (i) from80 to 95 weight % vinyl acetate residue, (ii) from 5 to 20 weight %ethylene residue, and (iii) from 0.1 to 5 weight % silane residue, withthe proviso that the sum of the weight % of the monomers equals 100; (b)a pigment composition including solids selected from the groupconsisting of inorganic pigments, inorganic fillers and mixtures thereofpresent in an amount such that the paint formulation has a pigmentvolume concentration (PVC) of from 25% to 85%; and (c) one or moreauxiliary components selected from the group consisting of wettingagents, dispersants, emulsifiers, protective colloids, thickeners,antifoams, dyes and preservatives; wherein (i) the resin has a K-valueof greater than 60, a latex gel content value upon curing at 125° C. for14 hours of greater than 50%, and a glass transition temperature (T_(g))of from about minus 5° to about plus 20° C. measured at a transitionmidpoint, and (ii) the paint formulation exhibits a relative scrub indexof greater than 200% and up to 300%; and wherein the resin and the paintformulation are alkylphenol ethoxylate (APE)-free.
 6. The water-based,low-emission paint formulation according to claim 5, wherein the VAEresin has a gel content value upon curing at 125° C. for 14 hours ofgreater than 60%.
 7. The water-based, low-emission paint formulationaccording to claim 5, wherein the VAE resin has a gel content value uponcuring at 125° C. for 14 hours of greater than 70%.
 8. The water-based,low-emission paint formulation according to claim 5, wherein the VAEresin has a gel content value upon curing at 125° C. for 14 hours ofgreater than 80%.
 9. The water-based, low-emission paint formulationaccording to claim 5, wherein the T_(g) of the resin is from minus 1° toplus 15° C. measured at a transition midpoint with a heating rate of 10K per minute.
 10. The water-based, low emission paint formulationaccording to claim 5, wherein the VAE resin exhibits a swelling ratio(S_(r)) value, upon curing at 125° C. for 7.5 minutes, of 2.5 to 3.5 inTHF.
 11. The water-based, low emission paint formulation according toclaim 5, wherein the VAE resin exhibits an S_(r) value, upon curing at125° C. for 7.5 minutes, of 2.5 to 3.5 in acetone.
 12. The water-based,low emission paint formulation according to claim 5, wherein the VAEresin exhibits an S_(r) value, upon curing at 125° C. for 14 hours, of2.5 to 4.0 in THF.
 13. The water-based, low emission paint formulationaccording to claim 5, wherein the VAE resin exhibits an S_(r) value,upon curing at 125° C. for 14 hours, of 2.0 to 3.5 in acetone.
 14. Thewater-based, low emission paint formulation according to claim 5,wherein the VAE resin exhibits an S_(r) value, upon curing at 125° C.for 14 hours, of 2.0 to 3.5 in ethyl acetate.
 15. A water-based,low-emission latex paint formulation containing a blend of a vinylacetate/ethylene (VAE) latex and an acrylic latex, wherein the blendcomprises: (a) 70 to 80 weight % of a vinyl acetate/ethylene (VAE)latex, based upon the total weight of the acrylic latex and the vinylacetate/ethylene latex, including a VAE resin comprising (i) from 80 to95 weight % vinyl acetate residue, (ii) from 5 to 20 weight % ethyleneresidue, and (iii) optionally from 0.1 to 5 weight % silane residue,with the proviso that the sum of the weight % of the monomers equals100; (b) 20 to 30 weight % of an acrylic latex, based upon the totalweight of the acrylic latex and the vinyl acetate/ethylene latex;wherein the paint formulation further comprises: (c) a pigmentcomposition including solids selected from the group consisting ofinorganic pigments, inorganic fillers and mixtures thereof present in anamount such that the paint formulation has a pigment volumeconcentration (PVC) of from 25% to 85%; and (d) one or more auxiliarycomponents selected from the group consisting of wetting agents,dispersants, emulsifiers, protective colloids, thickeners, antifoams,dyes and preservatives; wherein the paint formulation exhibits arelative scrub index of greater than 200% and up to 300% and theformulation is characterized in that (i) the VAE resin exhibits a glasstransition temperature (T_(g)) of from about minus 5° to about plus 20°C. measured at a transition midpoint and a K-value of greater than 60;and wherein the resin and the paint formulation are alkylphenolethoxylate (APE)-free.
 16. The water-based, low-emission latex paintformulation according to claim 15, wherein the acrylic latex comprisesthe emulsion polymerization product of at least one monomer selectedfrom the group consisting of methyl acrylate, ethyl acrylate, butylacrylate, 2-ethyl hexyl acrylate, decyl acrylate, methyl methacrylate,butyl methacrylate, iso-butyl methacrylate, iso-bornyl methacrylatehydroxy ethyl acrylate and hydroxy ethyl methacrylate.
 17. Thewater-based, low-emission latex paint formulation of claim 15, whereinthe acrylic latex includes vinyl acetate residue.
 18. A water-based,low-emission latex paint formulation comprising: (a) a vinylacetate/ethylene (VAE) latex including a VAE resin with from 80 to 95weight % vinyl acetate residue and from 5 to 20 weight % ethyleneresidue, optionally including additional monomers; (b) a pigmentcomposition including inorganic solids selected from inorganic pigments,inorganic fillers and mixtures thereof present in an amount such thatthe paint formulation has a pigment volume concentration (PVC) of from25% to 85%; and (c) one or more auxiliary components selected from thegroup of wetting agents, dispersants, emulsifiers, protective colloids,thickeners, antifoams, dyes and preservatives; wherein the latex,pigment composition, and auxiliary components are selected and utilizedin amounts such that the paint formulation exhibits a relative scrubindex of greater than 200% and up to 300%; and wherein the resin and thepaint formulation are alkylphenol ethoxylate (APE)-free.
 19. Thewater-based, low-emission paint formulation according to claim 18,wherein the VAE resin incorporates from 0.1 to 5 weight % of the residueof at least one monomer selected from the group consisting of silanemonomers, glycidyl acrylate, glycidyl methacrylate, allyl glycidylether, vinyl glycidyl ether, vinylcyclohexene oxide, limonene oxide,myrcene oxide, caryophyllene oxide, vinyltoluenes and styrenessubstituted with a glycidyl radical in the aromatic moiety,vinylbenzoates substituted with a glycidyl radical in the aromaticmoiety, acetoacetoxyethyl acrylate, acetoacetoxypropyl methacrylate,acetoacetoxyethyl methacrylate, acetoacetoxybutyl methacrylate, 2,3-di(acetoacetoxy)propyl methacrylate, and allyl acetoacetate.
 20. Thewater-based, low-emission paint formulation according to claim 18,wherein the VAE resin incorporates from 0.1 to 5 weight % of the residueof at least one monomer selected from the group consisting of glycidylacrylate, glycidyl methacrylate, allyl glycidyl ether, vinyl glycidylether, vinylcyclohexene oxide, limonene oxide, myrcene oxide,caryophyllene oxide, vinyltoluenes and styrenes substituted with aglycidyl radical in the aromatic moiety, and vinylbenzoates substitutedwith a glycidyl radical in the aromatic moiety.